System and method for impurity detection in beverage grade gases

ABSTRACT

A system and method for determining impurities in a beverage grade gas such as CO2 or N2 relies on a coupling of FTIR analysis and UV fluorescence detection. Conversion of reduced sulphur present in some impurities to SO2 can be conducted using a furnace. In some cases, CO2 % also is determined.

RELATED APPLICATIONS

This application claims the benefit under 35 USC 119(e) of U.S.Provisional Application No. 62/466,697, filed on Mar. 3, 2017, and U.S.Provisional Application No. 62/468,573, filed on Mar. 8, 2017, bothbeing incorporated herein by reference in their entirety.

BACKGROUND OF THE INVENTION

Carbon dioxide (CO₂) is a colorless, odorless gas that can be used as aninert material, as pressurized gas, in “dry ice”, liquid orsupercritical fluid applications, and many other areas, such as, forinstance, oil production and the chemical industry. In the food sector,CO₂ is a medium for decaffeination and a feedstock for obtainingcarbonated beverages, providing effervescence to water, soft drinks,wine, beer and so forth. Applications such as found in the beverageindustry require CO₂ of a specified purity. It is important, therefore,to monitor the nature and levels of contaminants in the gas employed.

Some existing systems for analyzing impurities in CO₂ gas rely on gaschromatography (GC), with photoionization detection (PID) and/or flameionization detection (FID). GC systems, however, can be slow, requiringseveral (e.g., 6-8) minutes between samples.

Other approaches rely on mass spectrometry (MS), a technique that isfast but can suffer from cross interferences and calibration issues. Aswith other MS systems, continued maintenance is often required.

Specialized instrumentation geared toward detecting a particularcontaminant (total sulfur, for instance) or a class of contaminants(e.g., aromatics) also have been developed. This approach, however,provides limited information. A sensor designed to focus on aromaticcompounds, for instance, may fail to signal the presence of acetaldehydeor nitrogen oxides (NO_(x)). One or more additional devices might beneeded to analyze for other contaminants. Combining multipleinstruments, however, can result in cumbersome calibrations andextensive maintenance.

SUMMARY OF THE INVENTION

A need continues to exist, therefore, for systems and techniques thatcan address problems associated with the approaches described above. Forgases used in the beverage industry, CO₂ or N₂, for example, there is aneed for systems and methods that can detect and measure a wide varietyof impurities (at parts per million (ppm) or even parts per billion(ppb) levels). In the case of CO₂, a need also exists for determiningthe quality of the gas being employed.

Generally, the invention combines Fourier transform infrared (FTIR) gasanalysis and UV fluorescence for measuring impurities in beverage gradegases.

Some of its aspects feature a system that comprises a FTIR component anda sulfur analyzer. The latter includes an oxidizing furnace forconverting reduced sulfur present in a gas sample to SO₂ and a UVfluorescence analyzer for measuring SO₂. The system can be fullyintegrated and, in specific implementations, can provide measurements ofCO₂ %, thereby assessing the quality of the CO₂ used.

Other aspects of the invention feature a method for measuring impuritiesin beverage grade gas such as CO₂, for example. In the method, a sampleis split between an FTIR analyzer and an apparatus designed to determinesulfur levels. The latter includes a furnace for converting reducedsulfur to SO₂. An ultraviolet (UV) fluorescence analyzer can be used tomeasure SO₂ levels.

Further aspects of the invention feature a system for measuringimpurities in a beverage grade gas. The system includes a FTIR analyzer,an oxidizing furnace for converting reduced sulfur present in a sampleto SO₂, and a manifold for directing the SO₂ from the oxidizing furnaceto the FTIR analyzer.

Embodiments of the invention present many advantages. In the beverageindustry, for example, the tolerance for many impurities is very low, inthe range of parts per million (ppm) or even parts per billion (ppb),for example. The system and method described herein can offer a fast andsensitive assessment of trace amounts while providing simultaneousreadings of multiple contaminants. Both organic (e.g., volatile organiccompounds or VOCs) as well as inorganic impurities such as total sulfur,sulfur oxides (SO_(x), e.g., SO₂) can be detected. Amounts of all thearomatics and aliphatics can be correctly summed up. Methane can bemeasured individually. Approaches described herein can detect andmeasure moisture, a critical contaminant that can be introduced duringtruck delivery. Levels of SO₂, total sulfur and total reduced sulfuralso can be determined.

While the existing approaches described above are not designed to giveinformation regarding the quality of the CO₂ gas, a quality that can beaffected by the presence of nitrogen gas (N₂) or air, the system andmethod described herein can measure and report CO₂ percentages in thegas being sampled.

The system offers faster measurement time, less calibration, analysis ofmore compounds, the capacity to measure multiple species and, in somecases, lower MDLs. In many instances the system offers a fullyintegrated impurity measurement system with a response times that can bedown to 5 seconds. Typically, the approaches described herein do notrequire calibrations for the FTIR data.

BRIEF DESCRIPTION OF THE DRAWINGS

In the accompanying drawings, reference characters refer to the sameparts throughout the different views. The drawings are not necessarilyto scale; emphasis has instead been placed upon illustrating theprinciples of the invention. Of the drawings:

FIG. 1 is a diagram of a system that can be used to detect impurities inbeverage grade gases.

FIG. 2 is a plot of CS₂ spiked concentrations obtained using embodimentsof the invention.

FIG. 3 is a plot of acetaldehyde spiked concentrations obtained usingembodiments of the invention.

FIG. 4 is a plot of benzene spiked concentrations obtained usingembodiments of the invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

The above and other features of the invention including various detailsof construction and combinations of parts, and other advantages, willnow be more particularly described with reference to the accompanyingdrawings and pointed out in the claims. It will be understood that theparticular method and device embodying the invention are shown by way ofillustration and not as a limitation of the invention. The principlesand features of this invention may be employed in various and numerousembodiments without departing from the scope of the invention.

As used herein, the term “and/or” includes any and all combinations ofone or more of the associated listed items. Further, the singular formsand the articles “a”, “an” and “the” are intended to include the pluralforms as well, unless expressly stated otherwise. It will be furtherunderstood that the terms: includes, comprises, including and/orcomprising, when used in this specification, specify the presence ofstated features, integers, steps, operations, elements, and/orcomponents, but do not preclude the presence or addition of one or moreother features, integers, steps, operations, elements, components,and/or groups thereof. Further, it will be understood that when anelement, including component or subsystem, is referred to and/or shownas being connected or coupled to another element, it can be directlyconnected or coupled to the other element or intervening elements may bepresent.

In many of its aspects, the invention relates to detecting impurities inbeverage grade gases, for instance impurities present in carbon dioxide(CO₂) gas and/or nitrogen gas (N₂). In some cases, total CO₂ amounts ina sample gas are determined as well.

CO₂ purity often depends on the CO₂ manufacturing process, plantpurification methods, storage, transportation, point of use conditionsand so forth. For the food and beverage sectors, for example, CO₂ isobtained via combustion, fermentation, from ammonia and hydrogenproduction. Both the preparation and the supply chain, often complex,that ultimately deliver the CO₂ to users can introduce impurities in theCO₂. Some of the contaminants particularly important to bottlers includeacetaldehyde, benzene, methanol, total sulfur content and totalhydrocarbons. Guidelines regarding CO₂ quality and best practices havebeen formulated by the International Society of Beverage Technologists®(ISBT), a group including beverage and CO₂ producers, distributors,providers of analytical and other related services and equipment.

The system and method described herein rely on a coupling of a Fouriertransform infrared (FTIR) gas analysis and UV fluorescence for measuringimpurities in beverage grade CO₂ and N₂, for example, or in otherapplications that place purity requirements on a gas. Examples ofimpurities that can be detected and quantified include but are notlimited to: SO₂, total sulfur, NH₃, CO, NO, NO₂, H₂O, HCN, CS₂, hydrogencyanide, methanol, moisture, acetaldehyde, methane, total hydrocarbons(methane, ethane, propane, pentane), benzene and total aromatichydrocarbons and others. In some implementations, the CO₂ % present inthe sample gas also is determined.

The FTIR spectrometer 16 can be, for instance, a MultiGas 2030 FTIR gasanalyzer with a 1 millimeter (mm) 7 micrometer (μm) TE-cooled detectormercury cadmium telluride (HgCdTe or MCT) detector, with a pressuretransducer rated to 6,000 Torr. While other detectors can be employed,the TE-cooled MCT detector does not require liquid nitrogen (LN2) andcan offer a better signal to noise ratio (SNR) than a standard 0.25 mmdetector. In comparison to the more conventional technology based ondeuterated triglycine sulfate (DTGS), MCT detectors are not as affectedby vibrations, since data collection is in the high kHz to MHz range.Specific examples employ a 9 micron (μm) cutoff detector that had a lowfrequency cutoff around 1,000 cm⁻¹. In other examples, use of a 7 μmTE-cooled MCT can provide an improvement in SNR by 3 to 5 times,resulting in 3 to 5 times lower minimum detection limits (MDLs), animportant feature for benzene which has the lowest MDL requirement of 20ppbv. MDL or Method Detection Limit is defined by the EnvironmentalProtection Agency (EPA) as the minimum concentration of a substance thatcan be measured and reported with 99% confidence that the analyteconcentration is greater than zero; it is determined from analysis of asample in a given matrix containing the analyte.

The cell 28 used by the FTIR spectrometer, also referred to as the “gascell” or “sample cell” can be made from a suitable material, forinstance welded stainless steel. In many embodiments, it is fabricatedto withstand pressures higher than atmospheric. In specific examples,the cell 28 is designed for pressures such as 2, 3, 4, 5 or higheratmospheres (atm) and 35° C. The cell 28 can be a flow through gas celldesigned for flow rates such as, for instance, 2 to 5 liters per minuteor 2000 to 3000 sccm (standard cubic centimeter per minute). Often, thesource pressure is considerably higher than the pressure in the gas celland a pressure regulator is included.

Increasing the pressure in gas cell 28 can improve sensitivity. Usinghigh pressures of CO₂ is feasible since CO₂ does not absorb strongly inthe spectral region in which impurities typically absorb. Thus, highamounts of CO₂ in the cell are not expected to interfere with thespectral features observed for the contaminants. Another gas that can bemonitored for impurities is N₂ With no absorption in the region ofinterest, even higher (above 5 atm, for example) pressures of N₂ can beintroduced in the cell, limited only by the materials and constructionof the cell.

Typically, the gas cell windows are BaF₂ or CaF₂ and for manyapplications they too are designed to handle pressures higher thanatmospheric, such as the pressures discussed above. Windows that are notwater sensitive and do not have high refractive indices are preferred.

Some embodiments utilize a multiple reflection gas cell, such as, forinstance, a White cell. Traditional White cells arrangements includethree spherical concave mirrors having the same radius of curvature.Modified White cells or other multiple path designs, e.g., Herriottcells, Pfund cells, cavity-ring down cells, and integrating spheres,also can be employed, as described by Spartz et al. in U.S. PatentApplication Publication No. 2015/0260695 A1, with the title Process andSystem for Rapid Sample Analysis, published on Sep. 17, 2015, now U.S.Pat. No. 9,606,088, both documents being incorporated herein by thisreference in their entirety. By increasing the path length traveled,multiple-pass arrangements can measure low concentration components ordetect weak absorption spectral features without increasing the physicallength or volume of the cell itself

Larger path lengths can be used in combination with higher reflectivecoatings such as enhanced silver.

In one non-limiting example, the gas cell 28 uses non-spherical concavemirrors to improve image quality and optical throughput. The mirrors arecut onto a single metal or a glass blank, providing a fixed path length;the mirrors can be the solid end caps of the gas cell, allowing forsmaller sample cells that are easier to align. For a White type cellwith a volume of about 200 mL, using gold mirrors can produce a pathlength of about 5.11 meters (m), while enhanced silver mirrors canresult in a path lengths of 10 m or longer.

In further examples, the sample cell is a light pipe flow through samplecell.

In many cases, the FTIR 16 is run at 4 cm⁻¹ resolution at about 5 seconddata collection with Triangle or other Apodization. A rolling average of1 to 5 minutes can be used with display updates at 5 to 6 secondintervals. A lower resolution, such as 8 cm⁻¹ resolution, might providesomewhat better MDLs for some of the compounds of interest like benzeneand the total aromatics. Using too low a resolution may result in lossesin the capability of measuring some of the narrow absorbing gases.

Configurations can be designed to obtain 1 ppb MDL for benzene. Allother compounds can be detected with improvements of 100 to 1000 overthe values required by the ISBT.

In practice, benzene often can be used as a surrogate for all aromaticimpurities. Since all the aromatic impurities absorb in the samespectral region (3000-3200 cm⁻¹ ) and can be measured as a group bymeasuring just one, it is possible to quantify for benzene and report asbenzene and total aromatic hydrocarbon content. Preferably, linearregression is used to determine the area under the spectral plot in thisaromatic region. In general, these aromatic compounds produced about thesame signal per MOL.

Light VOCs such as methane, ethane, propane and pentane can be measuredfor the aliphatic hydrocarbons (most are in the 2750-3000 cm⁻¹ region).

In many instances, an FTIR with a multiple pass White cell has a largedynamic range over 0 to 500 ppm; accuracy/linearity/ drift of +/−1%; CO₂measurement of 100% +/−0.1%; MDL for impurities of 1-3 ppb; and MDL fortotal sulfur of 1 ppb.

Another implementation utilizes technology that combines the separationpower of chromatography with the quantification power of absorptionspectroscopy, as described, for example by U.S. Pat. No. 9,606,088. Thisapproach can be particularly useful in detecting VOCs, for example.

In many cases the FTIR spectrometer 16 is provided with calibrations fora large number of impurities. Others can be added.

One approach described herein only measures impurities in a CO₂ sample.Another measures not just contaminants but also the amount of CO₂present in the CO₂ sample gas, (CO₂ %). The latter determination isperformed by having a high purity CO₂ source, for obtaining a referencemeasurement, or a high purity CO₂ calibration spectrum resident on thecomputer, e.g., in a calibration database, which can be compared withthe collected spectra. The results can show whether the gas is lowquality, containing, for example, significant amounts of N₂ or O₂.

In addition to measuring CO₂ %, the calibration also serves to removethe CO₂ spectral features while quantifying the impurities. Thisspectrum must match closely or errors will occur in the analysis for theimpurities.

In some examples, a source of ultrahigh purity CO₂ 80 be added in orderto supply the system with a high purity reference gas.

Turning to contaminants that contain sulfur, an oxidizing furnace(operating at a suitable temperature, e.g., 980° C.) is employed toconvert all the reduced sulfur to SO₂. Total sulfur is measured by UVfluorescence and includes any SO₂ initially present in the sample alongwith the SO₂ generated by the oxidizing furnace from reduced sulfurcompounds (e.g., H₂S, CH₃SH, CS₂, COS (carbonyl sulfide), (CH₃)₂S,(CH₃)₂S₂, and so forth).

The FTIR spectrometer 16 can measure SO₂ directly, so the amount ofreduced sulfur can be calculated by comparing the FTIR reading with thatobtained from the sulfur UV fluorescence analyzer 14.

In practice, the CO₂ is mixed with CDA (Clean Dry Air) to oxidize allthe sulfur compounds. In some embodiments, one or both streams (i.e.,CDA and/or the CO₂ gas sample) is/are preheated, to a suitabletemperature, prior to entering the furnace 18, to facilitate theoxidation reaction. Suitable means for heating the gases include heatexchangers, heating tape, heating jackets, ovens, Peltier heaters,cartridge heaters, and so forth. It is also possible to preheat a streamobtained by combining (mixing) CDA and CO₂. In many cases, the gasstream(s) will be at a temperature within a range of from roomtemperature, to a temperature that is equal to or lower than thetemperature of the furnace.

The UV fluorescence analyzer 14 may need to be calibrated occasionally,so a permeation tube with COS is present in the analyzer to calibratethe instrument. An example of existing technology designed to measuretotal reduced sulfur compounds and sulfur dioxide (SO₂) is theEnvironment S.A. AF22M-TRS Analyzer, available from Altech EnvironmentU.S.A. This instrument is capable of monitoring sulfur compounds, suchas, for example, H₂S, CH₃SH, CS₂, COS, (CH₃)₂S, (CH₃)₂S₂, and can workin three selectable modes: cyclic SO₂/TRS, continuous SO₂ and continuousTRS. In specific examples, a permeation tube 20 is provided as part ofthe TRS analyzer.

In another approach, the oxidation furnace 18 s used to generate theSO₂, essentially as described above, but in this embodiment theresulting SO₂ is directed to the FTIR analyzer 16 rather than to the UVfluorescence instrument. The UV fluorescence analyzer 14 can thus bebypassed or even eliminated from the overall system, the latter optionresulting in reducing costs and a streamlined design. Calibrationrequirements would be reduced or eliminated (due to the FTIR detection).On the other hand, eliminating the UV fluorescence analyzer 14 mayincrease measurement times, as one gas would need to be measured, thenthe other. Effecting changes in pressure between the FTIR and the sulfurdetermination may lead to sensitivity losses and add complexity.

The system has one and preferably more than one sample inputs, tohandle, for example, truck delivery, bulk and purified bulk samples.Automatic switching between the various channels can be provided. Inmany cases, input process gas streams from different points of thecarbonation process or plant (e.g., delivery tanker, pre- orpost-filtration and so forth), along with zero gas and validation gasare controlled. If desired, the system and method described herein canbe integrated with the plant design.

FIG. 1 is a diagram of one illustrative implementation of a system thatincludes a FTIR analyzer 16, a furnace 18 utilized for TRSdeterminations and a UV fluorescence analyzer 14. Also included areconduits and equipment for directing gases and for controlling pressuresand flows used in operating the system 10.

More specifically, shown in FIG. 1 is system 10 including: TRS converter12, UV fluorescence analyzer 14, and FTIR spectrometer 16.

TRS converter 12 includes furnace 18, where, in the presence of heat andan oxidizing gas such as oxygen, sulfur-containing compounds yield SO₂.Typically, the SO₂ output from the furnace and, more generally from theTRS converter unit, will include (i) SO₂ present as such in the samplegas, and (ii) SO₂ generated through the conversion taking place in thefurnace.

TRS converter 12 can be provided with permeation device 20 and severalrestrictors, e.g., 22 a, 22 b, 22 c and 22 d. Inputs 31, 33 and 35 canbe used for introducing, respectively, the CO₂ sample, a CO₂ referencegas (ultra-pure CO₂, for example) and CDA. Other elements may bepresent, as known in the art. In some cases, TRS converter 12 is acommercial apparatus or a unit thereof.

SO₂-containing output from furnace 18 and more generally from TRSconverter 12 (stream 24, for example) can be directed to UV fluorescenceanalyzer 14 (capable of measuring SO₂ levels and thus determining atotal SO₂ amount (including initial SO₂ present in the sample as SO₂ andSO₂ obtained by converting sulfur-containing impurities in furnace 18).In some cases, UV fluorescence analyzer 14 also can be used to measureSO₂ levels directly, e.g., SO₂ levels present in a gas sample, acalibration or reference gas or a purge gas. Using the twodeterminations, amounts of impurities containing reduced sulfur can beobtained by subtracting the measurement of initial SO₂ present as suchin the sample gas from the measurement of SO₂ in the output obtainedfrom furnace 18.

The fluorescence analyzer 14 includes cell 11, pump 13 and regulator 15.Filter 26, containing activated charcoal, for instance, can be used totrap gas contaminants such as, for example, aromatic hydrocarbons. Othercomponents can be included, as known in the art. In many cases, UVanalyzer 14 is a commercial unit or part of a commercial unit. In oneexample, the UV analyzer is a Model AF22M UV analyzer.

In some embodiments, UV fluorescence analyzer 14 is bypassed oreliminated and the output from furnace 18 (and more generally from TRSconverter 12) is directed to FTIR analyzer 16 using, for example, amanifold including suitable conduits, valves, flow controls, pressureregulators and/or other devices.

FTIR spectrometer 16 (e.g., a MultiGas 2030 FTIR apparatus) includessample cell 28. As described above, sample cell 28 can be configured asa multiple path cell, a White or modified White cell, for example. Inspecific embodiments, the cell is configured to withstand pressureshigher than atmospheric.

System 10 further includes various arrangements for supplying anddirected gases to one or more of the units (modules) described above,namely to the TRS converter, the UV fluorescence analyzer and/or FTIRanalyzer. Source 40, for instance, provides the CO₂ gas sample beingevaluated. The pressure of the sample gas can be reduced, e.g., from 275psig (pounds per square inch gauge) to 105 psig, using pressureregulator 42. In general, for best performance, the pressure of the gasinside the instrument 10 is in the range of ______.

The sample is split, conduits, valves, regulators, flow controls andother devices being provided for directing part of the sample CO₂ to TRSconverter 12 and another part to FTIR analyzer 16. In the arrangementshown in FIG. 1, a first CO₂ portion enters the TRS converter 12 at aflow rate of 40 liters per hour (LPH) after passing through pressureregulator 44 and valve 46. A second CO₂ portion is conducted through asuitable valve 48, a ⅔ port solenoid valve for water, air and vacuum,for example, and mass flow controller (MFC) 50 to enter FTIR analyzer 16at a flow rate of 5 liters per minute (LPM) through FTIR inlet 17.

If desired, a portion of the CO₂ sample being analyzed can be fed to theUV fluorescence analyzer for a direct measurement of initial SO₂ levelspresent in the sample.

Clean dry air (CDA) is brought in from source 60, via pressure regulator62 and valve 64 to provide O₂ for TRS converter 12. In one example, itspressure is reduced from 105 psig to 17.4 psig; an initial flow rate ofabout 6 LPM is decreased first to about 0.5 to 1.2 LPM, entering TRSconverter 12 (input 35) at a flow rate of 10 LPH.

CDA also can be used in FTIR analyzer 16. For example, a portion of theCDA stream exiting pressure regulator 62 is used to purge the FTIRoptics, entering the FTIR analyzer at a flow rate of, e.g., 0.5 LPM,through FTIR purge inlet 19. Another portion of CDA can be split beforethe CDA stream enters pressure regulator 62 and can be directed to flowcontrol 50 and FTIR analyzer 16 via valve 66, e.g., a ⅔ port solenoidvalve for water, air and vacuum, or another suitable device. Valve 61can be used to adjust the pressure of the CDA obtained from CDA source60.

In conjunction with a CDA purifier (e.g., a suitable purifier modelobtained from Parker Hannifin Corp.), not shown in FIG. 1, purified CDAcan be used as zero and purge for the FTIR. Other implementations employN₂ for zeroing and for purging the FTIR.

In some examples, system 10 is configured to supply a reference CO gas,e.g., from source 80, a gas tank, for example, that can be used in theanalysis of the CO₂ sample from source 40. In one example, the referenceCO₂ gas is an ultra-high purity CO₂ gas. In another example, thereference CO₂ gas is used for calibration purposes, e.g., to introduce aknown amount of COS to the TRS converter (e.g., via pressure regulator71 and valve 73). Further implementations utilize a purification device(carbon filter or another suitable trap) capable of removingcontaminants present in the CO₂ sample gas and generate purified CO₂gas. The latter can be used as the reference CO₂, in the FTIR analyzer,for example.

System 10 includes various vents (see, e.g., vents 90, 92 and 94) forthe release of gases from the various units (modules) discussed above.Vent 94 is used in conjunction with pressure regulator 96 to address theabove atmospheric pressure (e.g., several atmospheres) of the gasexiting gas cell 28 through FTIR outlet 21. Bypass conduit 23 isprovided with valve 25.

The system can include control system 120, typically a computer systemfor collecting, analyzing and reporting the data. Other features thatcan be provided include touch screen technology, PLC and MFC control ofgas streams, multiple (e.g., 4) automated sample channels, pressurecontrols for CO₂, N₂ and/or CDA inputs. Ethernet, Modbus and/or othercan be used for data communication and remote control.

In one example, operation of a system such as system 10 is conducted asfollows.

Before a sample is collected both analyzers are zeroed either by CDA orN₂ This can take place once a day, more frequently or at other suitableintervals.

The CO₂ sample is introduced into the system from one of several (i.e.,two or more) locations from a facility or plant that uses CO₂. In oneexample, the CO₂ sample is provided from one of up to four (4) locationsat the plant. The system automatically selects the gas to be analyzed orthe selection can be made manually by the user. The chosen sample issplit between the FTIR analyzer and the sulfur analyzer, in manyembodiments the TRS converter 12. The pressure to the FTIR is maintainedat 5 atm, while the sample to the converter 12 is dropped to a fewpounds per square inch gauge (psig).

The FTIR sample is constantly being measured by the FTIR every 5 to 6seconds and reported. The data are normally averaged from 1 to 5 minutesto lower the MDLs and remove process fluctuations. The FTIR reports CO₂% and all the impurities except total sulfur.

Reference CO₂ that is ultra-pure can be utilized to obtain a baselineFTIR spectrum. This reference CO₂ 80 can be a separate cylinder ofknown-pure gas or can be the sample CO₂ that has been passed throughcarbon filters.

In specific examples, the reference CO₂ in the FTIR sample cell ismaintained at a pressure higher than atmospheric, e.g., a pressure thatis the same or similar to the pressure of the sample CO₂ in the gascell. IR features of the reference CO₂ can be subtracted from the IRfeatures of the sample CO₂, resulting in spectral features that can beused to identify impurities.

If reference CO₂ 80 has water, the spectral signatures of theseinterference can be subtracted from the reference spectra for the pureCO₂. Care must be taken, however, to avoid negative concentrations.Specifically, the reference spectrum is reviewed for any positivebiases.

Alternatively or additionally, calibrations for high purity CO₂ can beresident on the computer system or accessible to it. For instance, CO₂calibration spectra can be available in a database.

The sulfur analyzer, e.g., using the UV fluorescence analyzer describedabove, generates a constant reported concentration that is also averagedover time. These data can be used to calculate total reduced sulfur bysubtracting the SO₂ initially present in the sample gas as SO₂, asmeasured by the FTIR.

FIGS. 2-4 are plots of typical impurities that were spiked into theprocess CO₂ to demonstrate the technique and technology as describedherein.

Further details are provided in the non-limiting example below.

EXAMPLE

In this example (referencing FIG. 1), the FTIR is provided with threesample options: (1) off: (2) zero: and (3) sample. The FTIR iscontrolled by a multi gas software suite such as, for example, theMG2000, reporting to a suitable display software via an AK Interface,for instance. Two solenoid valves (elements 48 and 66 in FIG. 1) and amass flow controller (MFC 50 in FIG. 1) control sample stream selectionand flow rates. When the instrument is in the “off” sample selection,both valves are closed and no gas reaches the FTIR 16. In the zerosample selection, the CDA or nitrogen valve 66 is opened and the MFC 50is set to a suitable flow rate such as, for example, 5,000 standardcubic centimeter per minute (sccm). After purging the system (e.g., for10-15 minutes) a new background can be taken in the MG2000 software.This background allows a clean reference single beam for comparison tonew sample data.

The instrument is then placed in sample mode, the nitrogen valve 66 isclosed and the CO₂ valve 48 is opened. The MFC remains set at 5,000sccm, however due to the composition of CO₂, a conversion factor of 0.7is applied to the total flow. Therefore the resultant flow is actually3,800 sccm. In the sample mode, the current single beam is compared tothe reference single beam and an absorbance spectrum is created.Absorbance spectra are analyzed via classical least squares (CLS)fitting to determine the level of contaminants present in the CO₂stream. Both the background and the sample are analyzed at 5 atm toeliminate difference due to pressure. The measurement at 5 atm isimportant as it allows a significant decrease in detection limits bypressuring the analysis (gas) cell. This can be controlled by a manualback pressure regulator that is set prior to the collection of thebackground or sample gases. Calibrations for all contaminant gases werecollected at the analysis conditions as well prior to deployment.Parameters associated with this configuration of the FTIR are summarizedin Table 1:

TABLE 1 (FTIR) Step Gas Flow (sccm) Pressure (ATM) Zero Nitrogen (N₂)5,000 5 Sample Carbon Dioxide (CO₂) 3,800 5

The TRS (total reduced sulfur) analyzer 12 used in this example also hasthree options: (1) Zero; (2) Span; and (3) Sample, and is controlled byits own independent software. The correct flow rates can be set viaregulators internal to the particular system. Once thermally stable, theTRS analyzer 12 is placed into zero mode, where the sample CO₂ isscrubbed via a charcoal filter to remove contaminants and then analyzed.The instrument zero value is taken via the internal reference zerofunction. Next, the instrument is placed into Span mode where thereference CO₂ is drawn across a permeation bench 20 to introduce a knownlevel of COS into the system. This then is converted to SO₂ via thefurnace 18 and measured by the instrument. The internal auto spanfunction corrects the calibration curve to the span response. Afterthese two calibration steps are conducted, the instrument is placed intosample mode where any sulfur species is converted to SO₂ and thenreported via the instrument. The calibration and measurement steps areperformed at ambient pressure (1 atm). Any sample stream switching iscontrolled by an integrated box, not the sulfur analyzer itself.

Table 2 shows a possible configuration for the TRS analyzer:

TABLE 2 (TRS Analyzer) Step Gas Flow (sccm) Pressure (ATM) Zero CarbonDioxide (CO₂), 667 1 scrubbed Span Carbon Dioxide (CO₂), 667 1Permeation Bench Sample Carbon Dioxide (CO₂) 667 1

The display is via a software program that can, for example, pullcurrent data from the MG2000 software via a suitable interface such as,for example, an AK interface and data from the TRS analyzer via a Modbusor another suitable protocol. It allows users to identify maximumallowable concentrations for all gases, warning percentages for a listof gases, and the amount of time to average data. Additionally, it caninclude controls for sample switching for the FTIR. After pulling in andaveraging the data, the concentrations of contaminants are displayed,and a graphical representation of the data can be shown via a bar charton the right. Both the concentration and its corresponding bar canchange between green, yellow, and red, for instance, based upon the usersettings for maximum concentrations and warning percentages.

In some cases, the software handles a single inlet sample. Other designscan sample between several (e.g., four or more) inlet streams. Infurther implementations, functionality is added to create an instrumentvalidation stream internal to the instrument that can allow users tomeasure a known concentration of gases via the FTIR to ensure theinstrument is working properly.

While this invention has been particularly shown and described withreferences to preferred embodiments thereof, it will be understood bythose skilled in the art that various changes in form and details may bemade therein without departing from the scope of the inventionencompassed by the appended claims.

What is claimed is:
 1. A system for measuring impurities in a beveragegrade gas, the system comprising: a FTIR component; and a sulfuranalyzer including an oxidizing furnace for converting reduced sulfurpresent in a sample to SO₂ and a UV fluorescence apparatus fordetermining total SO₂ amounts in the sample.
 2. The system of claim 1,wherein the FTIR component includes a gas cell that is a multiple pathtype cell.
 3. The system of claim 1, wherein the FTIR component includesa gas cell configured for pressures higher than atmospheric.
 4. Thesystem of claim 1, further comprising a computer for collecting,analyzing and/or reporting data.
 5. The system of claim 1, furthercomprising software for collecting, analyzing and/or reporting data. 6.The system of claim 1, further comprising calibration information forpure CO₂ and/or one or more impurity.
 7. The system of claim 1, whereinthe FTIR component is provided with a mercury cadmium telluridedetector.
 8. A method for analyzing a beverage grade gas, the methodcomprising: directing a first portion of a gas sample to a FTIR gascell; measuring impurities present in the gas cell; directing a secondportion of the gas sample to an oxidizing furnace; converting reducedsulfur present in the second portion to SO₂, and measuring a total SO₂in the second portion of the gas sample.
 9. The method of claim 8,wherein the total SO₂ is the sum of SO₂ initially present in the secondportion of the gas sample and SO₂ converted from reduced sulfur.
 10. Themethod of claim 8, wherein total SO₂ measured in the second portion ofthe gas is compared with SO₂ measured by FTIR in the first portion ofthe gas sample to determine a TRS amount.
 11. The method of claim 8,wherein data obtained for impurities in the first portion of the gassample are compared with calibration data.
 12. The method of claim 8,wherein a CO₂ % in the first portion of the gas sample is determined byFTIR and compared to calibration information.
 13. The method of claim 8,wherein the first portion of the gas sample in the gas cell is at apressure higher than atmospheric pressure.
 14. The method of claim 8,wherein the impurities are selected from the group consisting of SO₂,total sulfur, NH₃, CO, NO, NO₂, H₂O, HCN, CS₂, hydrogen cyanide hydrogencyanide, methanol, moisture, acetaldehyde, methane, total hydrocarbons,benzene and total aromatic hydrocarbons.
 15. The method of claim 8,wherein the gas sample is obtained from a location in a plant.
 16. Themethod of claim 8, wherein the beverage grade gas is CO₂ or N₂.
 17. Themethod of claim 8, wherein total SO₂ is measured by UV fluorescence orby FTIR spectrometry.
 18. A system for measuring impurities in abeverage grade gas, the system comprising: a FTIR analyzer; an oxidizingfurnace for converting reduced sulfur present in a sample to SO₂; and amanifold for directing the SO₂ from the oxidizing furnace to the FTIRanalyzer.
 19. The system of claim 18, wherein the FTIR analyzer includesa gas cell.
 20. The system of claim 18, wherein the gas cell is amultiple pass type cell.
 21. The system of claim 18, wherein the gascell is a flow through gas cell.